EP1003757A1

EP1003757A1 - Method for producing metallocenes

Info

Publication number: EP1003757A1
Application number: EP98942609A
Authority: EP
Inventors: Andreas Winter; Carsten Bingel; Volker Fraaije; Frank Kueber
Original assignee: Targor GmbH; Basell Polyolefine GmbH
Current assignee: Basell Polyolefine GmbH
Priority date: 1997-07-28
Filing date: 1998-07-23
Publication date: 2000-05-31
Anticipated expiration: 2018-07-23
Also published as: US6319874B1; JP4118507B2; EP1003757B1; JP2001510847A; ES2191962T3; WO1999005153A1; DE59807082D1

Abstract

The invention relates to a method for producing rac/meso metallocenes, the rac/meso metallocenes themselves, and their use in the production of isotactic polyolefins.

Description

Process for the production of metallocenes

description

The present invention relates to a process for the preparation of rac / meso-metallocenes, the rac / meso-metallocenes themselves and the use of the rac / meso-metallocenes as a catalyst component for the preparation of isotactic polyolefins.

Racemic metallocenes (rac-metallocenes) with partially hydrogenated or hydrogenated p-ligands are catalyst precursors for the polymerization of olefins, for example in J. Organomet. Chem. 497 (1995) 181, Angew. Chem. 104 (1992) 1373, Organometallics 12 (1993) 4391 or Chem. Ber. 127 (1994) 2417, J. Am. Chem. Soc. 118 (1996) 2105, Macromolecules 27 (1994) 4477 or Macromolecules 29 (1996) 2331, EPA 0 344 887, J. Mol. Catal. A. Chem. 102 (1995) 59, EPA 0 185 918, EPA 0 537 686, EP 0 485 820 or EP 0 485 821.

In the synthesis of metallocenes, the isolation of the racemic form of the metallocene is elaborately sought, since only with this form, for example, isotactic polypropylene can be produced. The meso form of the metallocene is separated off. In the production of metallocenes with partially hydrogenated or hydrogenated p-ligands, the racemic form of the unhydrogenated metallocene is first isolated and then hydrogenated. For example, from rac-Dimethylsilandiylbisinde- nyl dichloride by hydrogenating the octahydro DirnethylsilandiyIbis- rac- (4,5,6, 7-tetrahydroindenyl) -zirkoniumdiChlo ^¬ rid be prepared. These and similar reactions are at ^¬ game as described in EPA 0344887, J. Organomet. Chem. 497 (1995) 181, Organometallics 10 (1991) 1501 or J. Organomet. Chem. 342 (1988) 21.

The known synthesis procedures for the hydrogenation of aromati ^¬ rule Ligandgerüsts of rac-metallocenes tread all the same way in principle. The purified rac-metallocene is dissolved or suspended in dichloromethane and hydrogenated in the presence of platinum black or platinum dioxide under high hydrogen pressure (cf. J. Organomet. Chem. 342 (1988) 21 or EPA 0 344 887).

Dichloromethane and other chlorinated solvents can only be used in large quantities in compliance with strict occupational safety and environmental regulations. In chlorinated solvents, only weakly activating hydrogenation catalysts such as platinum black or platinum dioxide can be used to avoid dehalogenation reactions. The dehalogenation reactions lead to decomposition of the product and to corrosion problems.

The object of the present invention is to provide an efficient, fast, inexpensive and yield-optimized direct synthesis of metallocenes, with which highly isotactic polyolefins can be produced inexpensively.

The object of the present invention is achieved by a process for the direct production of rac / meso-metallocenes with tetrahydroindenyl ligands. The rac / meso-metallocenes produced according to the invention can surprisingly be used directly as a catalyst component for olefin polymerization without additional, cost-intensive and yield-reducing isolation of the rac form being necessary.

Accordingly, a process for the preparation of a rac / meso-metalocene of the formula I with a rac / meso ratio of> 20: 1 to <200: 1 was found,

meso rac

formula 1

in which

M stems of the elements means a metal of groups IIIb, IVb, Vb or VIb of the Periodensy ^¬ and preferably a Group IVB metal such as Ti, Zr or Hf, particularly preferably Zr and Hf,

the radicals X are the same or different, preferably the same, and a hydrogen atom, a -C-C ₄ o-carbon-containing group such as -C-Cιo-alkyl, Ci -Cι ₀ -alkoxy-, C ₆ -C ₀ -aryl-, C ₆ -C ₂ o-aryloxy, C-C ₁₀ alkenyl, C ₇ -C ₄₀ arylalkenyl, C ₇ -C ₄ o-alkylaryl or

C ₈ -C ₄₀ arylalkenyl group, an -OH group, a halogen atom or a pseudohalogen such as nitrile, where linear or mixed branched -CC-alkyl and halogen atoms are preferred and chlorine and methyl are very particularly preferred,

the radicals R ¹ and R ^{2 are the} same or different, radicals with the same indexing may also be different, and a hydrogen atom, a C ₄ -C ₄ -carbon-containing group such as C 1 -C ₄ -alkyl, C 1 -C -o Alkoxy-, C ₆ -C ₂ o-aryl-, C ₆ -C ₂₀ -aryloxy-, C ₂ -Cι ₀ -alkenyl-, C ₇ -C ₄ o-arylalkenyl-, C -C ₄ o -alkylaryl- or C ₈ -C o-arylalkenyl group, an -OH group, a halogen atom or a pseudohalogen such as nitrile, or an NR ⁵ ₂ , OSiR ⁵ ₃ or PR ⁵ ₂ radical with R ⁵ in the meaning of X mean , wherein preferably the radicals R ^{2 are} identical and represent a hydrogen atom and the radicals R ^{1 are} identical and represent hydrogen or linear or branched C 1 -C 1 -alkyl,

B represents a bridge between the indenyl ligands, which can be, for example, one to four members, with one and two member bridges being preferred

containing the steps:

a) reaction of a substituted cyclopentadiene of the formula A with a

Bridging reagent BY ₂ to a bridged biscyclopentadienyl ligand system,

b) reaction of the bridged biscyclopentadienyl ligand system with a metal halide to give a metallocene of the formula Ia

c) hydrogenation of the metallocene of the formula Ia to a metallocene of the formula Ib

d) and optionally the reaction of a metallocene of the formula Ib with an organometallic compound R ³ M ^X to a metallocene of the formula Ic

whereby all steps are carried out in the same solvent or solvent mixture. The invention also relates to chiral rac / meso metallocenes of the formula I with a rac / meso ratio of> 20: 1 to <200: 1

Formula I.

in which

M denotes a metal from groups IIIb, IVb, Vb or VIb of the periodic table of the elements and preferably denotes a metal from group IVB such as Ti, Zr or Hf, particularly preferably Zr and Hf,

the radicals X are the same or different and are a hydrogen atom, a C ₁ -C ₄ o -carbon-containing group such as Cχ-Cχo-alkyl, Cι-Cιo alkoxy, C ₆ -C ₂₀ aryl, C ₆ -C ₂₀ - Aryloxy, C ₂ -C ₀ alkenyl, C ₇ -C ₄ o-arylalkenyl, C ₇ -C ₄ o-alkylaryl or C ₈ -C ₄ o-arylalkenyl group, an -OH group Halogen atom or a pseudohalogen such as nitrile, linear or branched Ci-Cio-alkyl and halogen atoms are preferred and chlorine and methyl are particularly preferred,

the radicals R ¹ and R ^{2 are the} same or different, radicals with the same indexing may also be different, and a water atom, a C ₄ -C ₄ -carbon-containing group such as Ci ^' Cio-alkyl -, Ci -Cio-alkoxy -, C ₆ -C ₂ o -Aryl -, C <-C ₂ o "aryloxy-, C ₂ -Cio -alkenyl -, C ₇ -C ₄₀ -arylalkenyl-, C ₇ -C ₄₀ -alkylaryl - or C ₈ C ₄₀ arylalkenyl group, an OH group, a halogen atom or a pseudohalogen such as nitrile, or an NR ⁵ ₂ , OSiR ⁵ ₃ or PR ⁵ radical with R ⁵ in the meaning of X, with preference being given to the radicals R ^{2 are} identical and represent a hydrogen atom and the radicals R ^{1 are} identical and represent hydrogen or linear or branched Ci-Cio-alkyl, B represents a bridge between the tetrahydro indenyl ligands, which can be, for example, one to four members, with one and two member bridges being preferred.

The invention also relates to a catalyst comprising a) at least one chiral rac / meso-metallocene of the formula I and b) at least one cocatalyst and the use of the catalyst for the polymerization of olefins or in a process for the polymerization of olefins.

In the process according to the invention, the ligand system is first prepared and the rac / meso-metallocene of the formula Ia is prepared without isolating the bridged bisindenyl ligand system, and then hydrogenated to the bis-tetrahydroindenyl-metallocene of the formula Ib. The rac / meso-metallocene of formal Ib can be further converted to the rac / meso-metallocene of formula Ic.

Scheme 1

5/2

5/3

rö ε CD

Λ um As illustrated in Scheme 1, a bridged bisindenyl system is produced in the process from an indene of the formula A after deprotonation with a strong base such as butyllithium or potassium hydride in a suitable solvent or solvent mixture after the addition of a bridging reagent BY. B is as defined in formula I and Y is a leaving group such as halogen. After further deprotonation with a strong base such as butyllithium or potassium hydride, the bridged bisindenyl system is treated with a metal halide from group Illb, IVb, Vb or VIb of the periodic table of the elements, preferably with the halides of titanium, zirconium and hafnium, particularly preferably with zirconium tetrachloride or hafnium tetrachloride converted to rac / meso-metallocene of the formula Ia. The metal halides can also be used as ligand-containing complexes such as HfCl (THF) ₂ , ZrCl ₄ (THF) ₂ , TiCl ₄ (THF) ₂ , TiCl ₃ (THF) ₃ , VC1 ₃ (THF) ₃ or ScCl ₃ (THF) _3rd

Bridge B is introduced by reacting the metalated indenyl with a compound of the formula BY ₂ . The BY ₂ compound is preferably a compound such as (CH ₃ ) ₂ SiCl ₂ , (CH ₃ ) (C ₆ H ₅ ) SiCl ₂ , CH ₂ Br ₂ , (CH ₃ ) ₂ CBr ₂ or 1,2 -Dibromo- ethane.

Alternatively, to introduce a Ci bridge, the corresponding benzofulvene can be reacted with an equivalent of the metalated indenyl. In these cases, B preferably denotes CH ₂ , C (CH ₃ ) _2; C (CH ₃ ) (C ₆ H ₅ ) and C (C ₆ H ₅ ).

Suitable solvents for the one-pot synthesis are aliphatic or aromatic solvents, such as, for example, hexane or toluene, preferably aromatic solvents, or ethereal solvents, such as, for example, tetrahydrofuran (THF), diethyl ether or dimethoxyethane (DME), and solvent mixtures from the abovementioned classes of solvents, for example Toluene / THF, toluene / DME, toluene / hexane / THF or hexane / diethyl ether.

After complex synthesis, the isolation of the rac / meso-metallocene of the formula Ia described above can follow or the reaction mixture containing rac / meso-metallocene is subjected directly to a hydrogenation.

To isolate the rac / meso-metallocene of the formula Ia, either the precipitated rac / meso-metallocene can be filtered off together with the inorganic salt formed or the rac / meso-metallocene is used in a sufficient amount 7 cenynthese solvent used, preferably an aromatic solvent such as. B. toluene in solution and separated from the resulting inorganic salt by filtration.

The rac / meso-metallocene isolated as a filter cake is optionally washed and dried. The rac / meso-metallocene can then be separated from salt-like components. The rac / meso-metallocene in solution is optionally freed from the solvent and isolated as a solid.

The rac / meso-metallocene obtained can be obtained in pure form or as a mixture with other constituents, such as inorganic salts.

Examples of the other constituents are inorganic salts such as LiCl, LiBr, NaCl, NaBr, KC1, KBr, MgCl ₂ , MgBr ₂ , MgBrCl, CaCl ₂ , A1C1 ₃ and filter aids such as Na ₂ S0, quartz powder and Celite. Other constituents can also be organic and organometallic secondary components. Organic secondary components are solvent residues, organic impurities from the starting materials, unreacted starting materials and incompletely converted intermediates in metallocene synthesis. Organometallic secondary components can be isomeric metallocenes, oligomeric metallocenes and those compounds which have been introduced by impurities in the starting compounds.

The rac / meso-metallocene of the formula Ia prepared can be converted directly to the corresponding tetrahydroindenyl derivative of the formula Ib. Hydrogenation of rac / meso-metallocene of the formula Ia as already described above in an aromatic or Sau ^¬ erstoffhaltigen aprotic solvent in the presence of minde ^¬ least a hydrogenation catalyst with hydrogen.

As solvent, aromatic solvents are referred to, the ten least one aromatic six-membered ring per molecule contained ^¬. Examples of aromatic solvents are benzene, toluene, xylene (as an isomer mixture),

o-xylene, m-xylene, p-xylene, mesitylene, tetralin, anisole, cumene, 1, 2-diethylbenzene, 1, 3-diethylbenzene, 1, 4-diethylbenzene, l-ethyl-2-methylbenzene, l-ethyl- 3-methylbenzene, l-ethyl-4-methylbenzene. Anisole, toluene, benzene, xylenes (as a mixture or pure substance) and tetralin are preferred.

The aprotic solvents containing oxygen include aromatic and aliphatic ethers such as anisole, ethylphenyl ether, isopropylphenyl ether, diethyl ether, di-n-butyl ether, tert-butyl ether 8 methyl ether, tetrahydrofuran, dioxane. In addition, esters of aliphatic or aromatic carboxylic acids can also be used as solvents, for example ethyl acetate and propyl butyrate.

The process described relates to a temperature range from 0 ° C to 150 ° C. In particular, the hydrogenation is carried out at 15 ° C to 100 ° C.

Suitable hydrogenation catalysts are compounds or elements which do not or only partially hydrogenate the solvent under the hydrogenation conditions used. Examples of such hydrogenation catalysts are palladium on activated carbon, palladium on barium sulfate, palladium on aluminum oxide, palladium black, palladium sponge, platinum oxide, platinum black, platinum sponge. Palladium catalysts, in particular palladium on activated carbon, are preferred.

The pure or hydrogenated rac / meso-metallocene of the formula Ib prepared above or mixed with other constituents can be further reacted with an organometallic compound R ³ M ¹ to give the rac / meso-metallocene of the formula Ic or used directly as a catalyst component in the polymerization become.

In the case of the compound R ¹ , M ^{1 is} an element from the 1st to 3rd main group, preferably lithium, magnesium or aluminum, and R ³ has the same meaning as X in formula I, except for halogen. If the rac / meso-metallocene of the formula Ia is to be isolable, particular preference is given to organometallic compounds in which the radical R ³ does not bear an aliphatically bound β-hydrogen atom. Examples of such compounds are lithium organyls such as CH ₃ Li, BenzylLi and CβHsLi, and Grignard compounds such as CH ₃ MgCl, CH ₃ MgBr, CH ₃ MgI, BenzylMgBr, C ₆ H ₅ MgCl and aluminum organyls such as trimethylaluminium or methylaluminoxane.

The reaction takes place in an opposite R ³ M ¹ ^¬ inert solvent or solvent mixture medium. Suitable solvents are aliphatic or aromatic solvents, such as, for example, hexane or toluene, ethereal solvents, such as, for example, tetrahydrofuran (THF), diethyl ether or dimethoxyethane (DME), and solvent mixtures from the abovementioned classes of solvents, such as, for example, toluene / THF, toluene / hexane / THF or hexane / The - ethyl ether.

The substitution of the halogen atoms on the transition metal is carried out at a temperature from -100 ° C. to the boiling point of the solvent or mixture used, preferably at a temperature 9 from -78 ° C to the boiling point of the solvent or mixture used.

After the reaction has taken place, the rac / meso-metallocene of the formula Ib can be separated, for example by extraction, from the metal halide formed and obtained by crystallization, the rac / meso ratio being able to change compared to the starting material.

Rac / meso-metallocenes of the silyl-bridged bis-tetrahydroindenyl complexes of hafnium or zirconium are preferably prepared as follows. 1 equivalent of indene is deprotonated at room temperature to 50 ° C. in a toluene / THF mixture 100: 1 to 1: 5, preferably 20: 1 to 2: 1 with a solution of n-butyllithium (preferably 1 equivalent) and then at - 30 ° C to room temperature with half an equivalent of an alkyl and / or aryl substituted dichlorosilane, such as. As dimethyldichlorosilane, added and stirred for 1 to 5 hours at a temperature between room temperature and 60 ° C. The mixture is then deprotonated with a further equivalent of butyllithium at room temperature to 50 ° C., stirring is continued for 1 to 5 hours at room temperature to 50 ° C. and at a temperature of -30 ° C. to 50 ° C., preferably -10 ° C. to room temperature, reacted with 0.4 to 1 equivalent, preferably 0.45 to 0.75 equivalents of the tetrachloride of zirconium or hafnium and then stirred for 1 to 5 hours. In the case of dimethylsilyl-bis-indenylzirconium dichloride, the complex suspension is filtered from the one-pot synthesis and washed with toluene or THF, preferably THF. The filter cake, which contains rac / meso dimethylsilyl-bisindenylzirconium dichloride, is suspended in toluene, palladium-on-carbon is added and the temperature is from 20 ° C. to 120 ° C., preferably 50 ° C. to 90 ° C. and a hydrogen pressure of 5 to 100 bar, preferably 10 to 50 bar hydrogenated. Rac / meso dimethylsilyl-bis (tetrahydro-inde- nyl) zirconium dichloride is separated from inorganic by-products by toluene extraction and is isolated as a solid after removal of a large part of the solvent.

Surprisingly, the new process has many advantages. The ligand synthesis and the complex synthesis to the rac / meso-metallocene of the formula Ia are carried out in the same reaction vessel and the same non-chlorinated solvents which are used in the subsequent hydrogenation to a rac / meso-metallocene of the formula Ib and which can be used in the substitution of the halogen atoms X on the transition metal M to a rac / meso-metallocene of the formula Ic. 10

By using non-chlorinated solvents, more effective hydrogenation catalysts can be used and the reactions can be carried out at relatively low hydrogen pressures. This is particularly interesting for technical applications. One avoids the chlorinated solvents, which are harmful from a safety and environmental point of view. The subsequent processing of the metallocenes is facilitated by using aromatic hydrocarbons or slightly polar aprotic solvents such as ether. In the preferred solvents such as anisole, toluene, benzene, xylene, tert. Butyl methyl ether and tetrahydrofuran can completely dissolve the product at elevated temperature, separate the hydrogenation catalyst and inorganic salt-like by-products and crystallize the product, or the solution can then be used directly as a catalyst component in the polymerization. The good solubility of the hydrogenated products in aromatic solvents at elevated temperature makes it possible to hydrogenate very concentrated metallocene suspensions, which is advantageous in view of a good space-time yield. In addition, compared to known processes, the amounts of hydrogenation catalyst required are considerably cheaper.

The present invention is illustrated by the following examples.

The rac / meso-metallocenes produced in the process according to the invention are compounds of the formula I in a rac / meso ratio of> 20: 1 to <200: 1, preferably> 30: 1 to <100: 1, particularly preferably of> 35: 1 to <60: 1, very particularly preferably> 40: 1 to <50: 1.

rac meso

Formula I. 11 being

M is a metal from the groups Illb, IVb, Vb ά v VIb dcu periodic table of the elements and preferably is a metal from the group IVb such as Ti, Zr or Hf, particularly preferably Zr and Hf,

the radicals X are the same or different, preferably the same, and a hydrogen atom, a -C-C ₄ o-carbon-containing group such as Ci-Cio-alkyl, Cι-Cιo alkoxy, C ₆ -C ₂₀ aryl, C ₆ -C ₂ o-aryloxy, C ₂ -Cι ₀ - alkenyl, C ₇ -C rj-arylalkenyl, C ₇ -C ₄ o-alkylaryl or C ₈ -C ₄ o-aryl-alkenyl group, a -OH group, a halogen atom or a pseudohalogen such as nitrile, it being possible linear or branched ^C ι ^_-Cιo alkyl and halogen atoms are preferred, and chlorine and methyl are most preferred,

the radicals R ¹ and R ^{2 are the} same or different, radicals with the same indexing may also be different, and a hydrogen atom, a C 1 -C ₄ o -carbon-containing group such as C 1 -C 10 -alkyl, C 1 -C 1 -alkoxy, C ₆ -C ₂₀ aryl, C ₆ -C ₂ o-aryloxy, C ₂ -Cι ₀ alkenyl, C ₇ -C ₄₀ arylalkenyl, C ₇ -C ₄₀ alkylaryl or C ₈ -C ₄₀ arylalkenyl group, an -OH group, a halogen atom or a pseudohalogen such as nitrile, or an NR ⁵ ₂ , SR ⁵ , OSiR ⁵ ₃ , SiR ⁵ ₃ or PR ⁵ radical with R ⁵ in the The meaning of X is, where the radicals R ² are preferably the same and represent a hydrogen atom and the radicals R ^{1 are the} same and are hydrogen or linear or branched Ci-Cio-alkyl,

B represents a bridge between the indenyl ligands, which can be, for example, one to four members, with one and two member bridges being preferred.

Examples of such bridges are

_R 14 »14 R ¹⁴ R« _R 14 _R 14 _R 14

I.

C - _O - W * - C —— «M2 ^ _ — _ C - C - C -

I.

_R 15, 15 _R 15 _R 15 _R 15 _R 15 _R 15 12

= BR ¹⁴ , = A1R ¹⁴ , -Ge-, -0-, -S-, = SO, = S0 ₂ , = NR ³⁴ , = CC, = P ¹⁴ or = P (0) R ¹⁴ , where R ¹⁴ and R ^{1 S} are the same verscheiden ouer and are a hydrogen atom, a halogen atom or a Cι-C _o-4 hydrocar- serstoffhaltige group such as a Ci-Cirj-, in particular 5 Cι-C ₄ alkyl group, a Cι-Cι ₀ fluoroalkyl , in particular CF ₃ group, a C ₆ -Cιo, in particular C ₆ -C ₈ aryl, a Cβ-Cio-fluoroaryl, in particular pentafluorophenyl group, a Ci-Cio, especially Cι ~ C alkoxy group, especially methoxy - group, a C -C -Co, especially C ₂ -C alkenyl group, a 0 C ₇ -C Q / especially C -Cιo arylalkyl group, a C ₈ -C ₄₀ , especially C ₈ -Cι ₂ arylalkenyl group, represent a C -C o-, in particular C -Ci ₂ -alkylaryl group or R ¹⁴ and R ¹⁵ each form a ring with the atoms connecting them and M ^{2 is} silicon, germanium or tin. 5

The bridge B preferably means

5 wherein M ^{2 is} silicon or germanium and R ¹⁴ and R ^{15 are the} same or different and are a -C-alkyl group or a C ₆ -C ~ aryl group.

_Q R ¹⁴ and R ¹⁵ are the same or different and are preferably hydrogen, a -CC alkyl group, in particular methyl group, CF ₃ group, C ₆ -C ₈ aryl, pentafluorophenyl group, Ci-Cio, -C-C _4th -Alkoxy group, in particular methoxy group, C ₂ -C ₄ alkenyl group, C ₇ -C ₁₀ arylalkyl group, C ₈ -Cι ₂ arylalkenyl group, 5 C -C ₂ alkylaryl group.

B is particularly preferably a bridge R ¹⁴ R ¹⁵ C =, R ¹⁴ R ¹⁵ Si = or - CR ¹⁴ R ¹⁵ -CR ¹⁴ R ¹⁵ -, where R ¹⁴ and R ^{15 are} identical or different and _{0 is} a hydrogen atom, a C 1. -C ₄ alkyl group or a Cβ-Cio-aryl group mean.

The particularly preferred rac / meso-metallocenes of the formula I have combinations of the following molecular fragments: 13

B: -CH ₂ -CH ₂ -, (H ₃ C) ₂ Si-- or (H ₃ C) ₂ C =, preferably (HjC); £ ^• =

MX ₂ : -ZrCl ₂ , -HfCl ₂ , -Zr (CH ₃ ) ₂ , -Hf (CH ₃ ) ₂

Ligand: tetrahydroindenyl

Examples of rac / meso-metallocenes of the formula I are mentioned below:

rac / meso-dimethylsilanediylbis (4,5,6,7-tetra-hydro-1-indenyl) zirconium dichloride rac / meso-dimethylmethylene bis (4,5,6,7-tetrahydro-l-indenyl) zirconium dichloride rac / meso-ethanediylbis ( 4,5,6,7-tetrahydro-l-indenyl) zirconium chloride rac / meso-dimethylsilanediylbis (4,5,6,7-tetra-hydro-1-indenyl) zirconium dimethyl rac / meso-dimethylmethylenebis (4,5, 6,7-tetrahydro-l-indenyl) zirconium dimethyl rac / meso-ethanediylbis (4,5,6,7-tetrahydro-l-indenyl) zirconium dimethyl rac / meso-dimethylsilanediylbis (4,5,6,7-tetra-hydro- 1-indenyl) hafnium dichloride rac / meso-dimethylmethylene bis (4,5,6,7-tetra-hydro-1-indenyl) hafnium dichloride rac / meso-ethanediylbis (4,5,6,7-tetrahydro-l-indenyl) hafnium dichloride rac / meso-dimethylsilanediylbis (4,5,6, 7-tetrahydro-l-indenyl) hafnium-dimethyl rac / meso-dimethylmethylene bis (4,5,6, 7-tetrahydro-l-indenyl) hafni- umdimethyl rac / meso-ethanediylbis (4,5,6,7-tetrahydro-l-indenyl) hafnium dimethyl

rac / meso-dimethylsilanediylbis (2-alkyl-4, 5, 6, 7-tetra-hydro-1-indenyl) zirconium dichloride rac / meso-dimethylmethylene bis (2-alkyl-4, 5,6, 7-tetra-hydro-1 -indenyl) zirconium dichloride rac / meso-ethanediylbis (2-alkyl-4, 5,6, 7-tetra-hydro-1-indenyl) zirconium dichloride rac / meso-dimethylsilanediylbis (2-alkyl-4, 5, 6, 7-tetra - hydro-1-indenyl) zirconium dimethyl rac / meso-dimethyl methylenebis (2-alkyl-4, 5,6, 7-tetra-hydro-1-indenyl) zirconium dimethyl rac / meso-ethanediyl bis (2-alkyl-4, 5,6 , 7-tetra-hydro-1-indenyl) zirconium dimethyl rac / meso-dimethylsilanediylbis (2-alkyl-4, 5,6, 7-tetra-hydro-1-indenyl) hafnium dichloride 14 rac / meso-dimethylmethylenebis (2-al yl-4, 5,6,7-tctra hydro-1-indenyl) hafnium dichloride rac / meso-ethanediylbis (2-alkyl-4, 5,6,7-tetra-hydro- 1-indenyl) hafnium dichloride rac / meso-dimethylsilanediylbis (2-alkyl-4, 5,6, 7-tetra-hydro-1-indenyl) hafniumdimethyl rac / meso-dimethylmethylene bis (2-alkyl-4, 5,6, 7- tetra-hydro-1-indenyl) hafniumdimethyl rac / meso-ethanediylbis (2-alkyl-4, 5,6, 7-tetrahydro-1-indenyl) hafnium dimethyl

In the case of the above-mentioned rac / meso-metallocenes, the rac / eso ratio is preferably> 30: 1 to <100: 1, particularly preferably> 35: 1 to <60: 1, very particularly preferably> 40: 1 to <50: 1 and alkyl is linear or branched Cι-Cι ₀ alkyl such as methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, tert-butyl, pentyl, isopentyl, hexyl or decyl.

The rac / meso-metallocenes according to the invention can surprisingly be used directly as a catalyst component for the production of highly iso-tactical polyolefins without the need to isolate the rac form. Such a catalyst system contains at least one cocatalyst and at least one rac / eso metallocene. Mixtures of metallocene can also be used, e.g. Mixtures of two or more rac / meso metallocenes of the formula I or mixtures of one or more rac / meso metallocenes of the formula I with one or more different metallocenes such as a bisindenyl metallocene which is substituted in the six-membered ring of the indenyl ligand. Such six-ring-substituted metallocenes are e.g. in EP-A-0 646 604. In addition, the rac / meso-metallocene can also be used in supported form for olefin polymerization.

The cocatalyst component which may be contained in the catalyst system contains at least one compound of the type of an aluminoxane or another Lewis acid or an ionic non-coordinating compound which converts this into a cationic compound by reaction with a metallocene. A compound of the general formula II is preferred as the aluminum inoxane

(R- A10) p (II)

used. Aluminoxanes can be cyclic as in Formula III 15

or linear as in Formula IV

or of the cluster type as in formula V, as described in more recent literature, cf. JACS 117 (1995), 6465-74, Organometallics 13 (1994), 2957-1969.

/

The radicals R in the formulas (II! Uli); iV) and (V) can be the same or different and a -C-C o-hydrocarbon group such as a Cχ-Cιo-alkyl group, one

C ₆ -C o-aryl group, or hydrogen, and p is an integer from 2 to 50, preferably 10 to 35.

The radicals R are preferably the same and are methyl, isobutyl, n-butyl, phenyl or benzyl, particularly preferably methyl. 16

If the radicals R are different, they are preferably methyl and hydrogen, methyl and ibobu.yl or methyl n-eutyl, with hydrogen or isobutyl or n-butyl preferably being present in an amount of 0.01 to 40% (number of the radicals R).

The aluminoxane can be made in various ways. According to a known method, an aluminum hydrocarbon compound and / or a hydridoaluminum hydrocarbon compound is reacted with water (gaseous, solid, liquid or bound - for example as crystal water) in an inert solvent, such as toluene. To produce an aluminoxane with different alkyl groups R, two different aluminum trialkyls (A1R ₃ + A1R ' ₃ ) are reacted with water according to the desired composition and reactivity (cf. S. Pasynkiewicz, Polyhedron 9 (1990) 429 and EP-A-302 424).

Regardless of the type of production, all aluminoxane solutions have in common a changing content of unreacted aluminum starting compound, which is present in free form or as an adduct.

In addition to aluminoxane, e.g. also understood other organoaluminum compounds or organoboron compounds which contain C 1 -C 20 carbon-containing groups, such as branched or unbranched alkyl or haloalkyl, such as methyl, propyl, isopropyl, isobutyl, trifluoromethyl, unsaturated groups, such as aryl or haloaryl, such as phenyl, Tolyl, benzyl groups, p-fluorophenyl, 3, 5-difluorophenyl, pentachlorophenyl, pentafluorophenyl, 3, 4, 5-trifluorophenyl and 3, 5-di (trifluoromethyl) phenyl.

Organoboron compounds are particularly preferred. Examples of such organic boron compounds are trifluoroborane, triphenylborane, tris (4-fluorophenyl) borane, ris (3, 5-difluorophenyDborane, tris (4-fluorophenyl) borane, tris (pentafluorophenylDborane, tris (tolyl) borane , Tris (3,5-dimethylphenyl) borane, tris (3,5-difluorophenyl) borane and / or tris (3,4,5-trifluorophenyl) borane, with particular preference being given to tris (pentafluorophenyl) borane.

Ionic non-coordinating cocatalysts are understood to mean, for example, compounds which contain a non-coordinating anion, such as tetrakis (pentafluorophenyl) borates, tetraphenyl borates, SbF ₆ -, CF ₃ S0 ₃ - or C10 ₄ -. Lewis acids such as methylamine, aniline, dimethylamine, diethylamine, N-methylaniline, diphenylamine, N, N-dimethylaniline, trimethylamine, tri - are used as the cationic counterion. 17 ethyiamine, tri-n-butylamine, Mothy.ldiphenylam.in, Pyridiπ, p-Bromc-N, N-dimethylaniline, p-Nitro-N, N-dimethylaniline, Trlethy Iphosphine, triphenylphosphine, diphenylphosphine, tetrahydrothiophene or tri-phenylcarbene .

Examples of such ionic compounds are triethylammonium tetra (phenyl) borate, tributylammonium tetra (phenyl) borate, trimethylammonium tetra (phenyl) borate, tributylammonium tetra (tolyl) borate,

Tributylammonium tetra (pentafluorophenyl) borate, tributylammonium tetra (pentafluorophenyl) aluminate, tripropylammonium tetra (dimethylphenyl) borate, tributylammonium tetra (trifluoromethylphenyl) borate, tributylammonium tetra (4-luorophenyl)

N, N-dimethylaniline tetra (phenyl) borate, N, N-diethylanilinium tetra (phenyl) borate,

N, N-dimethylanilinium tetrakis (pentaf luorophenyl) borate,

N, N-dimethylanilinium tetrakis (pentafluorophenyl) aluminate, di (propyl) ammonium tetrakis (pentafluorophenyl) borate,

Di (cyclohexyl) ammonium tetrakis (pentafluorophenyl) borate, triphenylphosphonium tetrakis (phenyl) borate, triethylphosphonium tetrakis (phenyl) borate, diphenylphosphonium tetrakis (phenyl) borate, tri (methylphenyl) phosphoniumetrakis (phenyl) borate, tri (dimylethyl borate), tri (phenylethyl borate), tri (phenylethyl borate), tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phenyl) borate, tri (phyl) pentafluorophenyl) borate, triphenylcarbenium tetrakis (pentafluorophenyl) aluminate, triphenylcarbenium tetrakis (phenyl) aluminate, ferrocenium tetrakis (pentaf luorophenyl) borate and / or ferrocenium tetrakis (pentafluorophenyl) aluminate.

Triphenylcarbenium tetrakis (pentafluorophenyl) borate and / or N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate are preferred. Mixtures of at least one Lewis acid and at least one ionic compound can also be used.

Borane or carborane are also cocatalyst components.

Compounds such as 7, 8-dicarbaundecarborane (13), undecahydrid-7, 8-dimethyl-dicarbaundecaborane,

Dodecahydrid-l-phenyl-1,3-dicarbonaborane,

Tri (butyl) ammonium decahydrid-8-ethyl-7, 9-dicarbaundecaborate,

4-carbanonaborane (14) bis (tri (butyl) ammonium) nonaborate,

Bis (tri (butyl) ammonium) undecaborate, bis (tri (butyl) ammonium) dodecaborate,

Bis (tri (butyl) ammonium) decachlorodecaborate,

Tri (butyl) ammonium-1-carbadecaborate, tri (butyl) ammonium-1-carba- 18 dodecaborates,

Tri (butyl) ammonium-l-trimethyxsilyl-l-cdrbάdecaborct e, tri (butyl) ammonium bis (nonahydrid-1, 3-dicarbonnonaborate) cobaltate (III), tri (butyl) ammonium bis (undecahydrid-7, 8-dicarbaundecaborate) ferrate (III) of importance.

The rac / meso-metallocene / cocatalyst system can be used unsupported or preferably also supported in the olefin polymerization.

The carrier component of the catalyst system according to the invention can be any organic or inorganic, inert solid, in particular a porous carrier such as talc, inorganic oxides or finely divided polymer powders such as polyolefins.

Inorganic oxides of elements from groups 2, 3, 4, 5, 13, 14, 15 and 16 are suitable, the periodic table of the elements. Examples of oxides preferred as carriers include silicon dioxide, aluminum oxide, and mixed oxides of the two elements and corresponding oxide mixtures. Other inorganic oxides that can be used alone or in combination with the last-mentioned preferred oxide carriers are MgO, Zr0 ₂ or B0 ₃ , to name just a few.

The carrier materials used have a specific surface area in the range from 10 m ² / g to 1000 m ² / g, a pore volume in the range from 0.1 ml / g to 5 ml / g and an average particle size from 1 μm to 500 μm. Carriers with a specific surface area in the range from 50 μm to 500 μm, a pore volume in the range between 0.5 ml / g and 3.5 ml / g and an average particle size in the range from 5 μm to 350 μm are preferred. Carriers with a specific surface area in the range from 200 m ² / g to 400 m ² / g, a pore volume in the range between 0.8 ml / g to 3.0 ml / g and an average particle size of 10 μm are particularly preferred up to 200 μm.

If the carrier material used naturally has a low moisture content or residual solvent content, dehydration or drying can be avoided before use. If this is not the case, as with the use of silica gel as a carrier material, dehydration or drying is recommended. The weight loss during glow (LOI = loss on ignition) should be 1% or less. The thermal dehydration or drying of the carrier material can be carried out under vacuum and at the same time with an inert gas blanket, such as nitrogen. 19

The drying temperature in the range is between 100 ° C and 1000 ° C, preferably between 200 ^C C and εθO ^'3 C. The pressure parameter is not decisive in this case. The duration of the drying process can be between 1 and 24 hours. Shorter or longer drying times are possible, provided that under the chosen conditions the equilibrium can be established with the hydroxyl groups on the support surface, which normally requires between 4 and 8 hours.

Dehydration or drying of the carrier material is also possible chemically by reacting the adsorbed water and the hydroxyl group on the surface with suitable inerting agents. As a result of the reaction with the inerting reagent, the hydroxyl groups can be completely or partially converted into a form which does not lead to any negative interaction with the catalytically active centers. Suitable inerting agents are, for example, silicon halides and silanes, such as silicon tetrachloride, chlorotrimethylsilane, dimethylaminotrichlorosilane, or organometallic compounds of aluminum, boron and magnesium, such as trimethyl aluminum, triethyl aluminum, triisobutyl aluminum, triethyl borane, dibutyl magnesium such as methyl or aluminoxane. The chemical dehydration or inertization of the carrier material can be carried out by reacting a suspension of the carrier material in a suitable solvent with the inerting reagent in pure form or dissolved in a suitable solvent with exclusion of air and moisture. Suitable solvents are aliphatic or aromatic hydrocarbons, such as pentane, hexane, heptane, toluene or xylene. The inerting takes place at temperatures between 25 ° C and 120 ° C, preferably between 50 ° C and 70 ° C. Higher and lower temperatures are possible. The duration of the reaction is between 30 minutes and 20 hours, preferably 1 to 5 hours. After the completion of the chemical dehydration, the support material is isolated by filtration under inert conditions, once or several times been described with suitable inert solvents as already previously be ^¬ are washed and then dried in a stream of inert gas or in a vacuum.

Organic support materials such as finely divided polyolefin powders such as polyethylene, polypropylene or polystyrene may also be used and should likewise be then freed by appropriate purification and drying operations before use of anhaf ^¬ tender moisture, solvent residues or other impurities. 20th

To display the supported catalyst analyzer system, for example, at least one of the rac / meεc metallocene components described above can be brought into contact with the cocatalyst component in a suitable solvent in order to obtain a soluble reaction product. The soluble reaction product is then added to the dehydrated or rendered inert material, the solvent removed, and the resulting supported rac / meso-metallocene catalyst system dried to ensure that all or most of the solvent is removed from the pores of the material. The supported catalyst is obtained as a free-flowing powder.

As an alternative to the carrier process described above, other addition sequences of rac / meso-metallocenes, cocatalysts and carriers are also possible.

A preferred method for the preparation of a free flowing and optionally prepolymerized supported catalyst system comprises the following steps

a) Preparation of a rac / meso-metallocene / cocatalyst mixture in a suitable solvent (preactivation), the rac / meso-metallocene component having one of the structures described above.

b) applying the preactivated rac / meso-metallocene / cocatalyst solution to a porous, generally inorganic, dehydrated support

c) removing most of the solvent from the resulting mixture

d) isolation of the supported catalyst system

e) If necessary, a prepolymerization of the supported catalyst system obtained with one or more olefinic monomer (s) in order to obtain a prepolymerized supported catalyst system.

Preferred solvents for the preparation of the preactivated rac / meso-metallocene cocatalyst mixture are solved hydrocarbon and hydrocarbon mixtures, the individual component temperature liquid at the chosen reaction Tempe ^¬ and in which preferable. The solubility of the individual components is, however, no prerequisite before ^¬ if it is ensured that the reaction product of rac / meso-metallocene and co-catalyst component selected in the 21

Solvent is soluble. Examples of suitable solvents include alkanes such as pentane, isopentane, hexane, Ke. tan, cctan, and nonane, cycloalkanes such as cyclopentane and cyclohexane, and aromatics such as benzene, toluene, ethylbenzene and diethylbenzene. Toluene is very particularly preferred.

The amounts of cocatalyst such as aluminoxane and rac / meso-metallocene used in the preparation of the supported catalyst system can be varied over a wide range.

In the case of aluminoxane, a molar ratio of aluminum to the transition metal in the rac / meso-metallocene of 10: 1 to 1000: 1 is preferably set, very particularly preferably a ratio of 50: 1 to 500: 1. In the case of methylaluminoxane, 30% toluene solutions are preferably used, the use of

15 10% solutions are also possible.

The rac / meso-metallocene according to the invention can be preactivated. For pre-activation, the rac / meso-metallocene can be dissolved in the form of a solid in a solution of the cocatalyst, such as aluminoxane, in a suitable solvent. It is also possible to dissolve the rac / meso-metallocene separately in a suitable solvent and then to combine this solution with the cocatalyst solution, such as aluminoxane solution. It is also possible to mix the rac / meso-5 metallocene-containing reaction mixture obtained in the metallocene synthesis with the cocatalyst solution, e.g. Combine aluminoxane solution. Toluene is preferably used. The pre-activation time can be approximately 1 minute to 200 hours. The preactivation can take place at room temperature (25 ° C). The use of higher temperatures can, in individual cases, shorten the time required for preactivation and cause an additional increase in activity. In this case, a higher temperature means a range between 50 ° C and 100 ° C.

5 The pre-activated solution can then be treated with an inert

Carrier material, usually silica gel, which is in the form of a dry powder or as a suspension in one of the abovementioned solvents. The silica gel is preferably used as a powder. The order of addition is arbitrary. The pre-activated metallocene cocatalyst solution can be metered into the support material or the support material can be added to the solution.

The volume of the preactivated solution can exceed 100% of the total pore volume of the carrier material used or up to 100% of the total pore volume. Preferred is because ^¬ at a range of 100 to 500%, particularly preferably from 110 to 22 300% of the total pore volume or 50% to 100% or preferably 70 to 95%.

The temperature at which the preactivated solution is brought into contact with the carrier material can vary between 0 ° C and 100 ° C. However, lower or higher temperatures are also possible. After the combination of carrier material and solution, the mixture is kept at this temperature for about 1 minute to 1 hour, preferably 5 minutes.

The solvent is then completely or largely removed from the supported catalyst system, and the mixture can be stirred and optionally also heated. Both the visible portion of the solvent and the portion in the pores of the carrier material are preferably removed. The solvent can be removed in a conventional manner using vacuum and / or purging with inert gas. During the drying process, the mixture can be heated until the free solvent has been removed, which usually requires 1 to 3 hours at a preferably selected temperature between 30 ° C. and 60 ° C. The free solvent is the visible proportion of solvent in the mixture. Residual solvent is the proportion that is enclosed in the pores.

As an alternative to a complete removal of the solvent, the supported catalyst system can also be dried only to a certain residual solvent content, the free solvent having been removed completely. Be dried Subsequently, the supported catalyst system can with a low boiling hydrocarbon radical such as pentane or hexane, and washed again ge ^¬.

The supported catalyst system can either be used directly for the polymerization of olefins or can be prepolymerized with one or more olefinic monomers before it is used in a polymerization process. For this purpose, for example, the supported catalyst system is suspended in an inert hydrocarbon such as hexane and at a temperature of 0 ° C to 60 ° C in the presence of at least one olefin such as ethylene, propylene, hexene, butene or 4-methyl-1- pentene prepolymerized. Subsequently, the pre-polymerized catalyst system can be up to free-flowing ability getrock ^¬ net. Alternatively, this suspension can also be used directly for the polymerization. Another possible Ausgestal - tung variant is the catalyst system in the gas phase ^¬ prepolymerize. To do this, stir at least one 23 olefin of the above meaning passed through the powder system present catalyst system.

A small amount of an α-olefin, such as styrene, as an activity-increasing component or an antistatic can be added as an additive during or after the preparation of the supported catalyst system.

The present invention also relates to a process for the preparation of a polyolefin by polymerizing one or more olefins in the presence of the catalyst system according to the invention comprising at least one rac / meso-metallocene of the formula I. The term polymerization is understood to mean homopolymerization and also copolymerization.

The supported catalyst system can be used as a scavenger for the polymerization of olefins in combination with an aluminum alkyl or an aluminoxane. The soluble aluminum components are added to the monomer and are used to purify the monomer from substances that can impair the catalyst activity. The amount of aluminum component added depends on the quality of the monomers used.

Olefins of the formula R ^a -CH = CH-R ^b are preferably polymerized, in which R ^a and R are identical or different and denote a hydrogen atom or a carbon-containing radical having 1 to 20 C atoms, in particular 1 to 10 C atoms, and R ^a and R ^b together with the atoms connecting them can form one or more rings.

Examples of such olefins are 1-olefins having 2 to 40, preferably 2 to 10, carbon atoms, such as ethene, propene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene or 1-octene, Styrene, dienes such as 1,3-butadiene, 1,4-hexadiene, vinyl norbornene, norbornadiene, ethyl norbornadiene and cyclic olefins such as norbornene, tetracyclododecene or methyl norbornene. In the process according to the invention, propene or ethene is preferably homopolymerized, or propene with ethene and / or with one or more 1-olefins having 4 to 20 C atoms, such as hexene, and / or one or more dienes having 4 to 20 C atoms such as 1, 4-butadiene, norbornadiene, ethylidene norbornene or ethyl norbornadiene. Examples of such copolymers are ethylene / propene copolymers or ethene / propene / 1,4-hexadiene terpolymers. 24

The polymerization is carried out at a temperature of -60 ° C to 300 ° C. preferably 50 ° C to 200 ° C, very particularly 50 ^D C to 33 ° C leads. The pressure is 0.5 bar to 2000 bar, preferably 5 bar to 64 bar.

The polymerization can be carried out in solution, in bulk, in suspension or in the gas phase continuously or batchwise, in one or more stages.

If necessary, hydrogen is added as a molecular weight regulator and / or to increase the activity.

The polymers produced with the catalyst system according to the invention have a uniform grain morphology and have no fine grain fractions. No deposits or caking occur during the polymerization with the catalyst system according to the invention.

With the catalyst system according to the invention, highly isotactic polyolefins, such as polypropylene, with high stereo and regiospecificity can be obtained.

The invention is illustrated by the following examples.

All glassware was heated in vacuo and flushed with argon. All operations were carried out in the absence of moisture and oxygen in Schlenk vessels. The solvents used were freshly distilled under argon over Na / K alloy and stored in Schlenk vessels.

It means:

VZ = viscosity number in cm ³ / g

M _w = molar mass weight average in g / mol (determined by gel permeation chromatography)

M _w / _n = molecular weight dispersity

Mp = melting point in ° C (determined with DSC,

20 ° C / min. Heating / cooling speed

II = isotactic index (II = mm + 0.5 mr) ni _SO = isotactic block length

(n _iso = 1 + [2 mm / mr])

II and ni _so determined by ¹³ C-NMR spectroscopy

Determination of the racrmeso ratio using 1H-NMR

Synthesis of rac / meso-metallocenes 25th

Example A

rac / meso-dimethylsilanediylbis (4, 5, 6, 7-tetra-hydro-1-indenyl) zirconium dichloride (1)

A solution of 50 g (387 mmol) of indene (90%) in 320 ml of toluene and 48 ml of THF was mixed with 150 ml (400 mmol) of a 20% solution of butyllithium in toluene at room temperature and stirred for one hour at room temperature. The suspension was then cooled to -10 ° C. and 23.5 ml (200 mmol) of dimethyldichlorosilane were added. After a one-hour stirring period, 150 ml (400 mmol) of a 20% solution of butyllithium in toluene were added and the reaction mixture was stirred for 1 hour. 46 g (197 mmol) of zirconium tetrachloride were added to the reaction mixture, the orange suspension was stirred for 2 hours at room temperature, filtered and washed with 100 ml of THF. The filter cake of rac / meso-dimethylsilanediylbisindenylzirconium dichloride was suspended in 500 ml of toluene together with 1.5 g (1.4 mmol) of palladium (10% on activated carbon) and hydrogenated at 70 ° C. and a hydrogen pressure of 20 bar. After 5 hours the reaction mixture was filtered hot, concentrated in half and crystallized at 0-5 ° C. 35.3 g (39% based on indene) of rac / meso-dimethyl-silanediylbis (4, 5, 6, 7-tetra-hydro-1-indenyl) zirconium dichloride (1) (rac / meso 38: 1) were obtained .

Polymerization examples

example 1

A dry 24 dm ³ reactor was rinsed with propylene and filled with 12 dm ³ liquid propylene and 25 cm ³ toluene methylaluminoxane solution (corresponding to 37 mmol Al, average degree of oligomerization was p = 22). The contents were stirred at 30 ° C for 5 minutes at 250 rpm. In parallel, 5 mg of the metallocene dimethylsilanediylbis (4,5,6,7-tetrahydro-l-indenyl) zirconium dichloride (from Example A, compound (1), rac / meso = 38: 1 mixture) were dissolved in 10 cm3 toluene methylaluminoxane solution ( 17 mmol AI) dissolved and preactivated by standing for 5 minutes. The solution was placed in the reactor and polymerized at 70 ° C for one hour.

2.03 kg of polymer were obtained. The metallocene activity was 406 kgPP / gMet. The following properties were determined on the polymer: VZ = 42 cm ³ / g; Molar mass Mw = 32500 g / mol, Mw / Mn = 1.9; Melting point 140 ° C; II = 94.8%; n _lso = 35. 26

Example 2

Representation of the supported K tal _/ satorsysLom:

86 mg 0.18 mmol) dimethylsilanediylbis (2-ethyl-l-indenyl) zirconium dichloride and 82 mg (0.18 mmol) dimethylsilanediylbis (4,5,6,7-tetrahydro-l-indenyl) zirconium dichloride (from Example A, rac / meso 38: 1) were dissolved at room temperature in 18 cm ³ (84 mmol Al) 30% toluene methylaluminoxane solution ¹ '. The mixture was diluted with 50 cm 3 of toluene and stirred at 25 ° C. for 10 min. 15 g of SiO ₂ ^{2) were} slowly introduced into this solution. After the addition had ended, the mixture was stirred for 5 min at room temperature. The mixture was then evaporated to dryness in vacuo at 40 ° C. in the course of 2 h and the residue was dried at 25 ° C. and 10 ^-3 mbar for 5 h. 23 g of a free-flowing, orange-pink powder were obtained which, according to elemental analysis, contained 0.16% by weight of Zr and 9.6% by weight of Al.

Polymerization:

A dry 16 dm ³ reactor, which had first been flushed with nitrogen and then with propene, was filled with 10 dm ^{3 of} liquid propene. 8 cm ^{3 of} 20% triethylaluminum solution in Varsol (Witco) were added as scavengers and the mixture was stirred at 30 ° C. for 15 min. A suspension of 1.5 g of the supported metallocene catalyst in 20 cm ^{3 of} Exxsol was then added to the reactor, heated to the polymerization temperature of 65 ° C. and the polymerization system was kept at 65 ° C. for 1 hour. The polymerization was stopped by venting the excess monomer and the polymer obtained was dried in vacuo. The result was 3.1 kg of polypropylene powder. The catalyst activity was 288 kg PP / (g Met xh) or 2.1 kg PP / (g Kat xh). The isotactic polypropylene shown had the following properties: mp 146 ° C; M _w = 180,000 g / mol, M _w / M _n = 3.6, VZ = 140 cm ³ / g, SD = 370 g / dm ³ ¹⁾ Albemarle Corporation, Baton Rouge, Louisiana, USA ²⁾ Silica type MS 948, WR Grace, Davison Chemical Division, Bal ^¬ timore, Maryland, USA, pore volume 1.6 ml / g, calcined at 800 ° C.

Example 3 Illustration of the supported catalyst system:

The batch from Example 2 was mixed with 113 mg (0.18 mmol) of dimethylsilanediylbis (2-methyl-4-phenyl-l-indenyl) zirconium dichloride and 82 mg (0.18 mmol) of dimethylsilanediylbis (4, 5, 6, 7-tetra-hydro-1 -indenyl) zirconium dichloride (from Example A, rac / meso 38: 1) repeated. The result was 24 g of a free flowing 27 red-orange powder which, according to the elementary analysis, contained 0.15% by weight of Zr and 10.1% by weight of Al.

Polymerization: The polymerization was carried out analogously to Example 2. The result was 3.2 kg of polypropylene powder.

The catalyst activity was 258 kg PP / (g Met xh) or 2.1 kg PP / (g Kat xh). The isotactic polypropylene shown had the following properties: mp 147 ° C; M _w = 480,000 g / mol, M _w / M _n = 4.7, VZ = 430 cm ³ / g, SD = 360 g / dm ³ .

Claims

28 patent claims

1. Process for the preparation of a rac / meso metallocene of the formula I with a rac / meso ratio of> 20: 1 to <200: 1

rac meso

Formula I.

in which

M denotes a metal from groups Illb, IVb, Vb or VIb of the periodic table of the elements,

the radicals X are the same or different and a hydrogen atom, a -C-C ₄ o-carbon-containing group such as Ci-Cio-alkyl, -C-Cιo-alkoxy, C ₆ -C ₂₀ aryl, C ₆ -C ₂₀ aryloxy, C ₂ -Cι ₀ alkenyl, C ₇ -C ₄ o-arylalkenyl, C ₇ -C ₄ o-alkylaryl or C ₈ -C ₄₀ arylalkenyl group, an -OH group, represents a halogen atom or a pseudohalogen such as nitrile,

the radicals R ¹ and R ^{2 are the} same or different, radicals with the same indexing may also be different, and a hydrogen tom, a C 1 -C ₄ o-carbon-containing group such as C 1 -C ₁₀ alkyl, C 1 -C ₁₀ alkoxy -, C ₆ -C ₂₀ aryl-, C ₆ -C ₂ o-aryloxy-, C ₂ -Cιo-alkenyl-, C ₇ -C ₄ o-arylalkenyl-, C ₇ -C ₄ o-alkylaryl- or C8 ^_ C ₄ o-arylalkenyl group, an -OH group, a halogen atom or a pseudohalogen such as nitrile, or an NR ⁵ ₂ , SR ⁵ , OSiR ⁵ ₃ , SiR ⁵ ₃ or PR ⁵ ₂ radical with R ⁵ in the meaning of X mean

B represents a bridge between the indenyl ligands,

containing the steps: 29 a) reaction of a substituted cyclpentaciens of the formula A with a

Bridging reagent BY ₂ to a bridged biscyclopentadienyl ligand system,

d) and optionally the reaction of a metallocene of the formula Ib with an organometallic compound R ³ M! to a metallocene of the formula Ic

whereby all steps are carried out in the same solvent or solvent mixture.

2. Chiral rac / meso metallocene of the formula I with a rac / meso ratio of> 20: 1 to <200: 1

Formula I.

in which 30th

M denotes a metal from the groups Illb, IVb, Vt> or Vl of the periodic table of the elements,

the radicals X are the same or different, and a hydrogen atom, a -C-C ₄ o-carbon-containing group such as

Ci-Cio-alkyl-, Ci-Cirj-alkoxy-, C ₆ -C ₂ o-aryl-, C ₆ -C ₂₀ -aryloxy-, C -C ₁₀ -alkenyl-, C ₇ -C ₄₀ -arylalkenyl-, Are C ₇ -C ₄₀ alkylaryl or C ₈ -C o-arylalkenyl, an -OH group, a halogen atom or a pseudohalogen such as nitrile,

the radicals R ¹ and R ^{2 are the} same or different, radicals with the same indexing may also be different, and a hydrogen atom, a C 1 -C ₄ o -carbon-containing group such as C 1 -C ₄ -alkyl, C 1 -C 1 -alkoxy, C ₆ -C ₂₀ aryl-, C ₆ -C ₂ o-aryloxy-, C ₂ -Cι ₀ -alkenyl-, C ₇ -C ₄ o-arylalkenyl-, C ₇ -C ₄ o -alkylaryl- or C ₈ -C ₄ o-arylalkenyl group, an -OH group, a halogen atom or a pseudohalogen such as nitrile, or an NR ⁵ -, SR ⁵ -, OSiR ⁵ ₃ -, SiR ⁵ ₃ - or PR ⁵ ₂ radical with R ⁵ in the meaning of X mean

B represents a bridge between the tetrahydro indenyl ligands.

3. Catalyst containing a) at least one chiral rac / meso-metallocene of the formula I according to claim 2 and b) at least one cocatalyst.

4. A catalyst according to claim 3 additionally containing a support.

Catalyst according to claim 3 or 4, in prepolymerized form.

6. A process for the polymerization of olefins in the presence of a catalyst according to one or more of claims 3 to 5.

7. Use of a catalyst according to one or more of claims 3 to 5 for the polymerization of olefins.